Estudios de la viabilidad y la vitalidad frente al congelado de la levadura probiótica Saccharomyces boulardii: efecto del preacondicionamiento fisiológico

The aim of this study was to evaluate the vitality and viability of the probiotic yeast Saccharomyces boulardii after freezing/thawing and the physiological preconditioning effect on these properties. The results indicate that the specific growth rate (0.3/h^?1) and biomass (2-3 × 10⁸ cells/ml) of S. boulardii obtained in flasks shaken at 28 °C and at 37 °C were similar. Batch cultures of the yeast in bioreactors using glucose or sugar-cane molasses as carbon sources, reached yields of 0.28 g biomass/g sugar consumed, after 10 h incubation at 28 °C; the same results were obtained in fed batch fermentations. On the other hand, in batch cultures, the vitality of cells recovered during the exponential growth phase was greater than the vitality of cells from the stationary phase of growth. Vitality of cells from fed-batch fermentations was similar to that of stationary growing cells from batch fermentations. Survival to freezing at –20 °C and subsequent thawing of cells from batch cultures was 0.31% for cells in exponential phase of growth and 11.5% for cells in stationary phase. Pre-treatment of this yeast in media with water activity (a_w) 0.98 increased the survival to freezing of S. boulardii cells stored at –20 °C for 2 months by 10 fold. Exposure of the yeast to media of reduced a_w and/or freezing/thawing process negatively affected cell vitality. It was concluded that stress conditions studied herein decrease vitality of S. boulardii. Besides, the yeast strain studied presented good tolerance to bile salts even at low pH values.     

Multi-parameter flow cytometry as a tool to monitor heterotrophic microalgal batch fermentations for oil production towards biodiesel

Multi-parameter flow cytometry was used to monitor cell intrinsic light scatter, viability, and lipid content of Chlorella protothecoides cells grown in shake flasks. Changes in the right angle light scatter (RALS) and forward angle light scatter (FALS) were detected during the microalgal growth, which were attributed to the different microalgal cell cycle stages. The proportion of cells not stained with PI (cells with intact cytoplasmic membrane) was high (> 90%) during the microalgal growth, even in the latter stationary phase, suggesting that the microalgal cells built-up storage materials which allowed them to survive under nutrient starvation, maintaining their cytoplasmic membranes intact. A high correlation between the Nile Red fluorescence intensity measured by flow cytometry and total lipid content assayed by the traditional lipid extraction method was found for this microalga, making this method a suitable and quick technique for the screening of microalgal strains for lipid production, optimization of biofuel production bioprocesses, and scale-up studies. The highest oil content (∼28% w/w dry cell weight, estimated by flow cytometry) was observed in the latter stationary phase. In addition, C. protothecoides oil also depicted the adequate fatty acid methyl ester composition for biodiesel purposes at this growth phase, suggesting that the microalgal oil produced during the latter stationary phase could be an adequate substitute for diesel fuel. Medium growth optimization for enhancement of microalgal oil production is now in progress, using the multi-parameter approach.     

Two-step process for initial capture of plasmid DNA and partial removal of RNA using aqueous two-phase systems

In this paper, a two-step process for initial capture of plasmid DNA (pDNA) and partial removal of RNA using polyethylene glycol (PEG) and di-potassium hydrogen phosphate aqueous two-phase systems (ATPS) has been investigated. A Kühni-type ATPS extraction column was prepared with 50 ml (12% (w/w) PEG 1450, 12% (w/w) phosphate) of stationary phase and loaded with crude mobile phase (26% (w/w) PEG 1450, 4% (w/w) phosphate and 70% (w/w) lysate) at a flow rate of 6 ml min⁻¹ at an impeller speed of 200 rpm. The experiment was terminated after 100 min, and after complete resettling of the phases, 45 ml of stationary phase was harvested. During a subsequent second extraction step contained 18% (w/w) PEG 300 and 14% (w/w) phosphate, a proportion of RNA, which was also concentrated during the column process, was removed. It was demonstrated that the recovery of pDNA in the second bottom phase was 89.4%, which was similar to the initial recovery after column extraction (92.1%).     

Correlations between reduction–oxidation potential profiles and growth patterns of Saccharomyces cerevisiae during very-high-gravity fermentation

When Saccharomyces cerevisiae was grown under three glucose concentrations (ca. 200, 250, and 300 g/l), controlled at three reduction–oxidation (redox) potentials (no control, −150 and −100 mV) by manipulating two aerations (0.82 and 1.3 vvm), we observed that the recorded redox potential profiles resembled bathtub curves, and the profiles correlated well to the growth patterns measured under the same conditions. According to the shape of bathtub curve, we subdivided the curve into four regions. Region I features an abrupt decline in redox potential (corresponding to the growth phase from lag and logarithmic to the onset of stationary phase) that correlates to rapid yeast propagation, resulting from fast glucose uptake. Region II (corresponding to the stationary phase in yeast growth, characterizes a constant level of redox potential) is maintained by proper sparging and constant agitation. The continual buildup of ethanol causes growth arrest of yeast, resulting in the reduction of net NADH production. As a result, an uprising of redox potential is the feature of Region III, which signifies the end of stationary phase followed by the commencement of death phase. The severity of growth environment due to ethanol toxicity results in a rapid decrease in yeast population. Region IV (corresponding to the death phase during yeast growth) characterizes a drastic reduction in yeast viability and a gradual leveling of redox potential. A low glucose feed correlates to a fast decline of redox potential, a small basin in the bathtub curve, short fermentation duration, and complete glucose utilization. Imposing the current redox potential settings to low glucose feeds exerts no appreciable effect on ethanol production. In contrast, a high glucose feed connects to a sluggish bathtub curve for all four regions and incomplete glucose utilization. Proximate analysis on carbon balance indicates that controlling redox potential at −150 mV and under ca. 250 and 300 g glucose/l conditions, gave the highest fermentation efficiency as compared to other conditions; but there were no beneficiary effect to control redox potential under ca. 200 g glucose/l conditions.     

High-pressure CO2 inactivation and induced damage on Saccharomyces cerevisiae evaluated by flow cytometry

The cultivability, integrity and permeabilisation of Saccharomyces cerevisiae in saline solution after high-pressure CO₂ treatment at 36 °C was assessed by using both conventional cultivation-based technique and flow cytometry. Conventional cultivation-based techniques do not allow the exact quantification of integer cells, which can be determined coupling the staining with propidium iodide and SYBR-Green I and the cell quantification by flow cytometry. A significant portion of cells injured by CO₂ treatment is incapable of forming colonies but is still integer and potentially metabolically active. The yeast cell damage was demonstrated to be dependent on the conditions applied. In particular the influence of different operative parameters on integrity and permeabilisation of yeast cells was evaluated: pressure (50–100 bar), treating time (10–20 min) and stirring rate (500–10,000 rpm). After a 20 min treatment at 100 bar, 36 °C and 10,000 rpm more than 95% of cells result with completely permeabilised membrane.     

Lactic acid bacteria isolated from fish gut produce conjugated linoleic acid without the addition of exogenous substrate

The production of conjugated linoleic acid (CLA) by four strains of lactic acid bacteria isolated from fish, i.e., Leuconostoc mesenteroides H20, Leuconostoc mesenteroides H22, Leuconostoc lactis H24 and Lactobacillus pentosus H16, was evaluated in MRS broth and on MRS agar. The bioconversion and production of CLA by resting cells were also assessed. Linoleic acid was detected in cultures grown on agar at percentages of up to 18.3% (w/w) of total fatty acid, and conjugated isomers were found in the fatty acid profiles of Lactobacillus pentosus H16. The percentage of CLA relative to total fatty acid increased from 5.68 ± 1.65% to 23.69 ± 0.79% when resting cells were removed from agar plates and incubated without the addition of exogenous linoleic acid as a substrate. When Lactobacillus pentosus H16 cells were incubated with linoleic acid, cyclization and changes in monounsaturated fatty acid percentages were observed instead of conjugation. These results show that growth on a solid support is required for CLA production. More significantly, an increase in the CLA content could be achieved by incubating resting cells without exogenous substrate.     

Anticancer mechanisms of action of two small amphipathic β2,2-amino acid derivatives derived from antimicrobial peptides

We have recently discovered that small antimicrobial β^2,2-amino acid derivatives (Mw < 500) also display activity against cancer cells. To explore their drug potential, we have presently investigated the mechanisms of action of two derivatives BAA-1 (IC₅₀ 8.1 μg/ml) and BAA-2 (IC₅₀ 3.8 μg/ml) on Ramos human Burkitt's lymphoma cells. Studies using annexin-V-FITC/propidium iodide staining and flow cytometry revealed essential mechanistic differences, which was confirmed by screening for active caspases, investigation of mitochondrial membrane potential, and electron microscopy studies. Our results indicated that BAA-1 killed Ramos cells by destabilizing the cell membrane, whereas BAA-2 caused apoptosis by the mitochondrial-mediated pathway.     

Zinc induced damage to kidney proximal tubular cells: Studies on chemical speciation leading to a mechanism of damage

This study was carried out to investigate whether zinc can potentiate renal toxicity using monolayer cultures of kidney proximal tubular cells and if so to establish the chemical species and the mechanism involved.MethodsZinc was prepared as the citrate complex at pH 7.4 in phosphate buffered saline. Monolayers of kidney proximal tubular cells under standard cell culture conditions were exposed to zinc concentrations of 0, 5 10, 20, 50 and 100 μmol/L. To assess cellular damage, thiazol blue (MTT) uptake, NAG and LDH release, DAPI staining and Tunel assay were used. Cytoprotective agents: trolox, cysteine, glutathione, ascorbic acid and sodium selenite were used to investigate if the damage was reversible.ResultsIncubation of kidney cells with zinc citrate showed a dose related reduction in cell viability (p < 0.005) associated with cellular uptake of zinc ions. After 24 h incubation with 100 μmol/L Zn citrate, NAG release was not significantly different compared to the control whereas LDH increased 3 fold. DAPI staining showed apoptotic bodies within the cells confirmed by Tunel assay using flow cytometry. Electron microscopy showed significant morphological changes including loss of brush border, vacuolated cytoplasm and condensed nuclei. Trolox almost completely (>85 ± 5%) and sodium selenite partially recovered (40 ± 4%) the viability of cells exposed to Zn but no protection was observed with other cytoprotectants, e.g. glutathione, cysteine or ascorbic acid.In conclusion zinc can induce damage to kidney cells by a mechanism dependent on zinc ions entering the cell, binding to the cell organelles and disrupting cellular processes rather than damage initiated by free radical and ROS production.     

Microbial biodegradable plastic production from a wheat-based biorefining strategy

Restructuring the current fermentation and recovery practices employed for the production of polyhydroxyalkanoates is essential for the commercialisation of environmentally benign and cost competitive biodegradable plastics. This study presents the potential of a wheat-based biorefinery for the production of poly(3-hydroxybutyrate) (PHB). Fed-batch bioconversions using Wautersia eutropha growing on wheat-derived media led to the production of 162.8 g/l PHB. A high PHB to total dry weight (TDW) yield of 93% (w/w) was achieved due to microbial autolysis at the end of fermentation. Images of bacterial cells taken with a Transmission Electron Microscope (TEM) indicated the potential of bacterial autolysis as a mean to shorten downstream processing for PHB purification. The consumption of amino acids and peptides derived from wheat gluten hydrolysis resulted in a high glucose to PHB conversion yield of 0.47 g/g. The respective yield regarding the amount of wheat used for the production of enzymes and PHB was around 0.3 g PHB/g wheat, which corresponds to 82.8% of the maximum theoretical conversion yield. The productivity achieved was around 0.9 g/l h. Fermentations carried out on wheat-derived media and media formulated with various commercial sources of nutrients (glucose, yeast extract, soy-protein acid hydrolysate, casein hydrolysates, corn steep liquor and various inorganic chemicals) showed that the proposed wheat-based biorefinery strategy enhanced PHB production.     

Evaluation of single cell oil from Aureobasidium pullulans var. melanogenum P10 isolated from mangrove ecosystems for biodiesel production

In this study, the yeast strain P10 which was identified to be a member of Aureobasidium pullulans var. melanogenum isolated from the mangrove ecosystems was found to be able to accumulate high content of oil in its cells. After optimization of the medium for lipid production and cell growth by the yeast strain P10, it was found that 8.0 g of glucose per 100 ml, 0.02 g of yeast extract per 100 ml, 0.02 g of ammonium sulfate per 100 ml, pH 6.0 in the medium were the most suitable for lipid production. During 10-l fermentation, a titer was 66.3 g oil per 100 g of cell dry weight, cell mass was 1.3 g per 100 ml, a yield was 0.11 g of oil per g of consumed sugar and a productivity was 0.0009 g of oil per g of consumed sugar per h within 120 h. At the same time, only 0.07 g of reducing sugar per 100 ml was left in the fermented medium. The compositions of the fatty acids produced were C_16:0 (26.7%), C_16:1(1.7%), C_18:0 (6.1%), C_18:1 (44.5%), and C_18:2 (21.0%). The biodiesel produced from the extracted lipid could be burnt well.     

Single cell oil production from hydrolysates of inulin and extract of tubers of Jerusalem artichoke by Rhodotorula mucilaginosa TJY15a

In this study, we found that Rhodotorula mucilaginosa TJY15a could accumulate 48.8% (w/w) oil from hydrolysate of inulin and its cell dry weight reached 14.8 g/l during the batch cultivation while it could accumulate 48.6% (w/w) oil and 52.2% (w/w) oil from hydrolysate of extract of Jerusalem artichoke tubers and its cell dry weight reached 14.4 g/l and 19.5 g/l during the batch and fed-batch cultivations, respectively. At the end of the fed-batch cultivation, only 0.04% of reducing sugar and 0.08% of total sugar were left in the fermented medium. Over 87.6% of the fatty acids from the yeast strain TJY15a cultivated in the hydrolysate of extract of Jerusalem artichoke tubers was C_16:0, C_18:1 and C_18:2, especially C_18:1 (54.7%). Therefore, the results show that hydrolysates of inulin and extract of Jerusalem artichoke tubers were also the good materials for single cell oil production.     

The simultaneous utilization of kinetic analysis and flow cytometry in the assessment of Lactobacillus rhamnosus ATCC 7469 physiological states produced by increasing oxygen limitation levels and lactic acid accumulation

Carbon limited continuous cultures of Lactobacillus rhamnosus ATCC 7469 were grown at dilution rates between 0.1 h⁻¹ and 0.6 h⁻¹. At 0.45 h⁻¹, oxygen uptake decreases producing a deficiency in the production of cell energy, lowering the concentration of biomass and finally accumulating glucose in the broth. Under the lack of energy pressure, L. rhamnosus ATCC 7469 triggers the production of lactic acid from pyruvate freeing NAD⁺ and stimulates glycolysis to continue, producing extra ATP from substrate-level phosphorylation. The 12-fold growing concentration of lactic acid and the 2-fold increase of succinic acid are in parallel with the steep 4-fold decrease of acetic acid production and small concentration changes of formic and propionic acids.The way the cells balance the available energy between the growing dilution rate and detoxification produces a stress within the culture, detected and described by flow cytometry. As the dilution rate increased, the proportion of L. rhamnosus ATCC 7469 cells with depolarized membrane steadily increased (1% at D = 0.20 h⁻¹, 8% at D = 0.30 h⁻¹, 14% at D = 0.45 h⁻¹ and 26% for D = 0.62 h⁻¹, respectively). Only a low level of 3.7% of the population did not recover from the demanding growth rates in the acidic environment.     

Synthesis of structured lipid with balanced omega-3: Omega-6 ratio by lipase-catalyzed acidolysis reaction: Optimization of reaction using response surface methodology

The present study deals with the production of structured lipid containing omega-3 and omega-6 fatty acids in the ratio of 1:1 by incorporating omega-3 fatty acids (α-linolenic acid) from linseed oil into groundnut oil using lipase (Lipozyme IM from Rhizomucor miehei) catalyzed acidolysis reaction in hexane. The reaction conditions were optimized by response surface methodology with a four-variable five-level central composite rotatable experimental design. The influence of four independent parameters, namely ratio of fatty acid concentrate from linseed to groundnut oil (0.66–1.98, w/w), reaction temperature (30–60 °C), enzyme concentration (1–5%) and reaction time (2–54 h) on omega-3 fatty acids incorporation into groundnut oil were optimized. Optimal conditions for the structured lipid containing omega-3 to omega-6 fatty acids in the ratio of 1:1 were determined to be; enzyme concentration 3.75% (w/w), temperature 37.5 °C, incubation time 30.81 h and ratio of free fatty acid concentrate from linseed oil to groundnut oil 1.16 (w/w).     

Metabolic engineering of Saccharomyces cerevisiae to improve 1-hexadecanol production

Fatty alcohols are important components of a vast array of surfactants, lubricants, detergents, pharmaceuticals and cosmetics. We have engineered Saccharomyces cerevisiae to produce 1-hexadecanol by expressing a fatty acyl-CoA reductase (FAR) from barn owl (Tyto alba). In order to improve fatty alcohol production, we have manipulated both the structural genes and the regulatory genes in yeast lipid metabolism. The acetyl-CoA carboxylase gene (ACC1) was over-expressed, which improved 1-hexadecanol production by 56% (from 45 mg/L to 71 mg/L). Knocking out the negative regulator of the INO1 gene in phospholipid metabolism, RPD3, further enhanced 1-hexadecanol production by 98% (from 71 mg/L to 140 mg/L). The cytosolic acetyl-CoA supply was next engineered by expressing a heterologous ATP-dependent citrate lyase, which increased the production of 1-hexadecanol by an additional 136% (from 140 mg/L to 330 mg/L). Through fed-batch fermentation using resting cells, over 1.1 g/L 1-hexadecanol can be produced in glucose minimal medium, which represents the highest titer reported in yeast to date.     

Toxin production,retention, and extracellular release by Dinophysis acuminata during extended stationary phase and culture decline

Dinophysis spp. produce diarrhetic shellfish poisoning (DSP) toxins and pectenotoxins. The extent to which the dinoflagellate cells retain their toxicity in stationary phase, a period when cells are most toxic, and their transition into cell death is not known. Here we present results on the production, recycling, retention, and release of toxins from a monoculture of Dinophysis acuminata during these two important stages. Once stationary phase was reached, cultures were divided between light and dark treatments to identify if light influenced toxin dynamics. Light was required for long-term cell maintenance (>2 months) of D. acuminata in the absence of prey, however, in the dark, cells in stationary phase survived on reserves alone for four weeks before beginning to decline. Cells maintained relatively constant levels of intracellular OA (0.39 ± 0.03 pg/cell, 0.44 ± 0.05 pg/cell), DTX1 (0.45 ± 0.09 pg/cell, 0.64 ± 0.10 pg/cell) and PTX2 (10.4 ± 1.4 pg/cell, 11.0 ± 1.9 pg/cell) in the dark and light treatments, respectively, throughout stationary phase and into culture decline. Toxin production was only apparent during late exponential and early stationary growth when cells were actively dividing. In general, the concentration of dissolved (extracellular) toxin in the medium significantly increased upon culture aging and decline; cells did not appear to be actively or passively releasing toxin during stationary phase, but rather extracellular release was likely a result of cell death. Light availability did not have an apparent effect on toxin production, quotas, or intracellular vs. extracellular distribution. Together these results suggest that a bloom of D. acuminata would retain its cellular toxicity or potency as long as the population is viable, and that cells under conditions of low light (e.g., at the boundary or below euphotic zone) and/or minimal prey could maintain toxicity for extended periods.     

Ursolic acid benzaldehyde chalcone,leads to inhibition of cell proliferation and arrests cycle in G1/G0 phase in colon cancer

The present study investigates the effect of matrine on colon cancer cell viability and apoptosis and tumor growth in mice xenograft model. The results from MTT assay revealed a concentration and time dependent reduction in viability of HCT8 and HT29 colon cancer cells by matrine. The viability of HCT8 and HT29 cells was reduced to 24.67 and 29.32% on treatment with 4 µM/ml concentration of matrine after 48 h (P < 0.05). The results from flow cytometry revealed increase in population of HCT8 and HT29 cells to 77.6 ± 0.3 and 54.0 ± 5.4%, respectively compared to 1.4 ± 0.3 and 2.4 ± 0.7% in control on exposure to 1 µM/ml concentration of matrine. Histone H2AX phosphorylation and expression of Myt1, cyclin A2, cyclin B1 and p53 were increased in HCT8 and HT29 cells on treatment with matrine for 48 h. Matrine treatment also increased the phosphorylation of cdc2 significantly compared to control cells at 48 h (P < 0.05). Results from Annexin-V/FITC-staining showed increase in proportion of apoptotic cells in HCT8 and HT29 cells 67.52 and 68.56 on treatment with 1 µM/ml of matrine. Matrine treatment caused a marked reduction in the growth of HCT8 cell xenograft after 21 days. Thus matrine inhibits cell viability, induces apoptosis and inhibits tumor growth in colon cancer.     

Efficient oleaginous yeasts for lipid production from lignocellulosic sugars and effects of lignocellulose degradation compounds on growth and lipid production

Microbial lipid production using lignocellulosic biomass is considered an alternative for biodiesel production. In this study, 418 yeast strains were screened to find efficient oleaginous yeasts which accumulated large quantities of lipid when cultivated in lignocellulosic sugars. Preliminary screening by Nile red staining revealed that 142 strains contained many or large lipid bodies. These strains were selected for quantitative analysis of lipid accumulation by shaking flask cultivation in nitrogen-limited medium II containing 70 g/L glucose or xylose or mixture of glucose and xylose in a ratio of 2:1. Rhodosporidium fluviale DMKU-SP314 produced the highest lipid concentration of 7.9 g/L when cultivated in the mixture of glucose and xylose after 9 days of cultivation, which was 55.0% of dry biomass (14.3 g/L). The main composition of fatty acids were oleic acid (40.2%), palmitic acid (25.2%), linoleic acid (17.9%) and stearic acid (11.1%). Moreover, the strain DMKU-SP314 could grow and produce lipid in a medium containing predominantly lignocellulose degradation products, namely, acetic acid, formic acid, furfural, 5-hydroxymethylfurfural (5-HMF) and vanillin, with however, some inhibitory effects. This strain showed high tolerance to acetic acid, 5-HMF and vanillin. Therefore, R. fluviale DMKU-SP314 is a promising strain for lipid production from lignocellulosic hydrolysate.     

Production of ω-hydroxyundec-9-enoic acid and n-heptanoic acid from ricinoleic acid by recombinant Escherichia coli-based biocatalyst

ω-Hydroxyundec-9-enoic acid and n-heptanoic acid are valuable building blocks for the production of flavors and antifungal agents as well as bioplastics such as polyamides and polyesters. However, a biosynthetic process to allow high productivity and product yield has not been reported. In the present study, we engineered an Escherichia coli-based biocatalytic process to efficiently produce ω-hydroxyundec-9-enoic acid and n-heptanoic acid from a renewable fatty acid (i.e., ricinoleic acid). Expression systems for catalytic enzymes (i.e., an alcohol dehydrogenase of Micrococcus luteus, a Baeyer–Villiger monooxygenase of Pseudomonas putida KT2440, an esterase of Pseudomonas fluorescens SIK WI) and biotransformation conditions were investigated. Biotransformation during stationary growth phase of recombinant E. coli in a bioreactor allowed to produce ω-hydroxyundec-9-enoic acid and n-heptanoic acid at a rate of 3.2 mM/h resulting in a final product concentration of ca. 20 mM. The total amount of ω-hydroxyundec-9-enoic acid and n-heptanoic acid produced reached 6.5 g/L (4.0 g/L of ω-hydroxyundec-9-enoic acid and 2.5 g/L of n-heptanoic acid). These results indicate that the high value carboxylic acids ω-hydroxyundec-9-enoic acid and n-heptanoic acid can be produced from a renewable fatty acid via whole-cell biotransformation.     

Optimized enzymatic synthesis of ascorbyl esters from lard using Novozym 435 in co-solvent mixtures

A mild and efficient method for the conversion of fatty acid methyl esters from lard into ascorbyl esters via lipase-catalyzed transesterification in co-solvent mixture is described. A solvent engineering strategy was firstly applied to improve fatty acid ascorbyl esters production. The co-solvent mixture of 30% t-pentanol:70% isooctane (v/v) was optimal. Response surface methodology (RSM) and central composite design (CCD) were employed to estimate the effects of reaction parameters, such as reaction time (12–36 h), temperature (45–65 °C), enzyme amount (10–20%, w/w, of fat acid methyl esters), and substrate molar ratio of fatty acid methyl esters to ascorbic acid (8:1–12:1) for the synthesis of fatty acid ascorbyl esters in co-solvent mixture. Based on the RSM analysis, the optimal reaction conditions were determined as follows: reaction time 34.32 h, temperature 54.6 °C, enzyme amount 12.5%, substrate molar ratio 10.22:1 and the maximum conversion of fatty acid ascorbyl esters was 69.18%. The method proved to be applicable for the synthesis of ascorbyl esters using Novozym 435 in solvent.